US723152A - Process of concentrating solutions. - Google Patents
Process of concentrating solutions. Download PDFInfo
- Publication number
- US723152A US723152A US334000A US1900003340A US723152A US 723152 A US723152 A US 723152A US 334000 A US334000 A US 334000A US 1900003340 A US1900003340 A US 1900003340A US 723152 A US723152 A US 723152A
- Authority
- US
- United States
- Prior art keywords
- milk
- freezing
- centrifugal
- product
- same
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title description 20
- 235000013336 milk Nutrition 0.000 description 18
- 239000008267 milk Substances 0.000 description 18
- 210000004080 milk Anatomy 0.000 description 18
- 238000007710 freezing Methods 0.000 description 13
- 230000008014 freezing Effects 0.000 description 13
- 239000000243 solution Substances 0.000 description 8
- 235000020186 condensed milk Nutrition 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 239000006071 cream Substances 0.000 description 5
- 238000010257 thawing Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000000470 constituent Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000012141 concentrate Substances 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 239000012595 freezing medium Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000002609 medium Substances 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 239000000110 cooling liquid Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 230000037213 diet Effects 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000000266 injurious effect Effects 0.000 description 1
- 239000006193 liquid solution Substances 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 235000020183 skimmed milk Nutrition 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
Images
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/14—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment
- A23C9/142—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration
- A23C9/1422—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration by ultrafiltration, microfiltration or diafiltration of milk, e.g. for separating protein and lactose; Treatment of the UF permeate
Landscapes
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Dairy Products (AREA)
Description
No. 723,152. PATENTED MAR. 17, 1903.
- A. GERBER.
PROCESS OF CONGENTRATING SOLUTIONS.
APPLICATION FILED JAN. 30, 1906. no MODEL.
3 4 4.: min/0;. i dim Am UNITED STATES AUGUSTMGURBER, or WURZBURG, GERMANY.
PROCESS OF CONCENTRATING SOLUTIONS.
SPECIFICATION forming part of Letters Patent No. 723,152, dated March 17, 1903.
Application filed January 30, 1900- $erial No. 3,340. (No specimens-l which Ihaveapplied forapatentin Germany, dated July 15, 1899; in Denmark, dated Angust 19, 1899; in England, dated August 24, l899,andin France,dated September11,1899,) of which the following is a specification.
The product hitherto known to the trade as condensed milk has the disadvantage of an unnatural taste, as well as a peculiar odor,
both of which are due to the methods of concentrating the same by evaporation as usually employed. Ordinarily the milk is subjected to prolonged boiling, and chemical changes are brought about by the heat which impair the nutritive value of the milk constituentsandimparta peculiar odor and taste, as of cooked milk. Furthermore, prolonged heating of the milk at comparatively high temperatures ruptures the fat-globules and renders the product not only more susceptible to deteriorating chemical changes, but imparts to the same a disagreeable unctuous or greasy taste. Also under such methods of preparation it is found necessary. to add a very considerable portion: of sugar. Such highly-sweetened condition not only unfits the product for many culinary purposes, but also renders the same highly injurious for use as a diet for infants.
By my improved method of concentrating or'oondensing milk I entirely dispense with the use of heat and produce an article that is odorless, has an unimpaired natural taste, will keep admirably, and in which the fatglobules'are preserved intact, the product being the natural milk minus a large proportion of its water. a
In order to avoid the objectionable defects common to condensed milk prepared by the ordinary well-known methods and to obtain a product having the desirableattributes enumeratedJproceed to carry out myinvention in the manner following,to wit: The fresh milk is first separated from the cream in the ordinary way by centrifugal action, the cream being reserved and added to the product later on. The skimmed milk is then placed in a suitable centrifugal machine, preferably having a central coil or chamber containinga refrigerating medium, such as ammonia, brine, or the like. The centrifugal machine is .then started, and as the freezing action proceeds the watery constituent of the milk is congealed into ice-crystals, which crystals are, by reason of their less specific gravity, displaced by the heavier solids and caused to accumulate about and adhere to the central coil or refrigerating-chamber, the more concentrated milk solution, deprived of a large portion of its water, finding its way to the outer periphery of the drum, whence it may be drawn 0K in any well'known manner. The product may be withdrawn at an intermediate stage of concentration and subjected to further similar treatment or the exit-valves may be so adjusted as to accomplish the desired high degree of concentration mono and the same continuous treatment .by subjecting the contents of the drum to the action of refrigeration and centrifugal separation during a sufiiciently-extended space of time. The mass of ice collected about the central refrigerating coil or chamber will in practice contain a certain amount of solid matter locked up between the crystals, varying with the nature of the liquid to be concentrated and the degree of centrifugal force applied. If it be desired to carry to its full extent the concentration of the matter undergoing treatment, the central mass of ice may be melted by the application of heat, as by the admission of steam to the refrigerating-coils, thus freeing any solid particles that may be inclosed within the ice, and then by repeated freezing under the influence of continued centrifugal force accomplish a further concentration. Such alternate freezing, thawing, and freezing may be continued untilthe solid matter is practically all separated from its watery constituent, when the concentra te may be withdrawn. After the withdrawal of the concentrated product the congealed water inthe form of ice may be removed by the application of steam or other convenient form of heat, when the drum will be ready for the condensing of other milk. After the withdrawal of the condensed milk from the apadded thereto and the product is ready for use. The condensed milk thus obtained differs from the article as ordinarily produced by evaporation in the particulars hereinbefore stated and may be diluted by the addition of water'to the original volume and will then have. the taste of fresh milk and will not exhibit the disagreeable odor or the unnatural sweetened taste and flavor of the ordinary condensed milk.
WhileI have herein described my process as applied to the concentration or condensing of milk as a typical example of its application, I desire it to be distinctly understood that I do not limit myself to the treatment of milk, as my process'is obviously valuable in the concentration of a great variety of liquids and solutions, and particularly those containing albumen and other substances which, like milk, are deleteriously aifected byv the heat in the 'ordin'arysprocess of concentrating by evaporation.
While my process is entirely separate and distinct from any particular form of apparatus adapted to the carying out of the same, yet for the purpose of illustration I have in the annexed drawings shown a preferr'ed form of centrifugal machine in which is supported centrally a coil or a chamber 6, adapted'to contain the refrigerating solution and which may or may not rotate with the drum, the said chamber or coil being provided with an inlet fand an outlet 9, as shown. As hereinbefore fully set out, when the refrigerating medium is admitted to the central coil or a stance, through the channels it, leading to an outlet 2' in'the axle b of the centrifugal machine-while the ice remaining may be melted by steam injected into said coils or chambers or applied to the exterior thereof.
In carrying out my process it will be understood that I may use centrifugal machines of various constructions, and I may subject the solution to the freezing medium necessary for the freezing outof the water, as-well as to' the heating agent necessary for. the thawing of the ice, in different ways. The freezing medium, moreover, may consist of any wellknown cooling liquid, gas, or the like, and
Letters Patent, is
may in some instances be applied directly to the solution.
Having thus fully described myinvention, what I claim as new, and desire to secure by 1. The process of treating solutions which consists in freezing out the watery constituents and simultaneously by centrifugal action effecting separation therefrom of the portion containing solids in concentrated form.
2. The process of efiecting a concentration of liquids, which consists in subjecting the same simultaneously to a freezing temperature and to centrifugal action thus elfecting a removal of the concentrate from the dilute portion.
3. The process of effecting a concentration of liquids, which consists in'subjecting the same simultaneously to centrifugal action and 'to a freezing temperature applied GED1- trally of the mass. I
4. The process of condensing milk, which consists in congealing the watery portion by refrigeration and at the same time by centrifugal'action efiecting a separation there, from of the portion containing solids.
5. The process of condensing milk,'which consists in subjecting the same to centrifugal action and simultaneously submitting the central portion'of the same to the influence of a freezing medium.
6. The process of condensing liquid solutions, which consists in alternately freezing and thawing the same while under the influence of centrifugal action.
7. The process of condensing milk, which consists in subjecting/the same simultaneously to a freezing temperature and to centrifugal action, then thawing the frozen portion and again freezing while under centrifnioo gal action. I
8. The process of condensing milk, which consists in removing therefrom the cream, then freezing out the watery constituent and simultaneously by centrifugal action elfectx05 ing a separation therefrom of the concentrate, and then adding to the concentrate the cream previously removed.
9. The process of producing condensed milk, which consists in' removing therefrom no the cream, alternately freezing and thawing the milkfwhile under the influence of continued centrifugal action, and then adding .the crea'mto the condensed product.
In witness'whereof I have hereunto set my :1 hand in' presence of two witnesses,
' AUGUST GURBER. Witnesses:
' HANS HUNGER, OSCAR BOOK.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US334000A US723152A (en) | 1900-01-30 | 1900-01-30 | Process of concentrating solutions. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US334000A US723152A (en) | 1900-01-30 | 1900-01-30 | Process of concentrating solutions. |
Publications (1)
Publication Number | Publication Date |
---|---|
US723152A true US723152A (en) | 1903-03-17 |
Family
ID=2791666
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US334000A Expired - Lifetime US723152A (en) | 1900-01-30 | 1900-01-30 | Process of concentrating solutions. |
Country Status (1)
Country | Link |
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US (1) | US723152A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2520939A (en) * | 1947-01-27 | 1950-09-05 | Inst Divi Thomae Foundation | Process of concentrating milk |
US2584345A (en) * | 1946-07-22 | 1952-02-05 | Charles F Hall | Convection-compensating centrifuge |
US2602745A (en) * | 1949-06-24 | 1952-07-08 | Ohio Commw Eng Co | Method of concentrating milk |
US2656276A (en) * | 1949-07-19 | 1953-10-20 | Ohio Commw Eng Co | Dried or evaporated food product, especially milk, and the process of making it |
US2705407A (en) * | 1950-02-10 | 1955-04-05 | John O Colonna | Sea water fractionation |
-
1900
- 1900-01-30 US US334000A patent/US723152A/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2584345A (en) * | 1946-07-22 | 1952-02-05 | Charles F Hall | Convection-compensating centrifuge |
US2520939A (en) * | 1947-01-27 | 1950-09-05 | Inst Divi Thomae Foundation | Process of concentrating milk |
US2602745A (en) * | 1949-06-24 | 1952-07-08 | Ohio Commw Eng Co | Method of concentrating milk |
US2656276A (en) * | 1949-07-19 | 1953-10-20 | Ohio Commw Eng Co | Dried or evaporated food product, especially milk, and the process of making it |
US2705407A (en) * | 1950-02-10 | 1955-04-05 | John O Colonna | Sea water fractionation |
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